CN106907271A - It is a kind of to reclaim the device that exhaust pipe of engine waste heat improves engine synthesis oil consumption utilization rate - Google Patents
It is a kind of to reclaim the device that exhaust pipe of engine waste heat improves engine synthesis oil consumption utilization rate Download PDFInfo
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- CN106907271A CN106907271A CN201710200333.2A CN201710200333A CN106907271A CN 106907271 A CN106907271 A CN 106907271A CN 201710200333 A CN201710200333 A CN 201710200333A CN 106907271 A CN106907271 A CN 106907271A
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- 239000002918 waste heat Substances 0.000 title claims abstract description 21
- 230000015572 biosynthetic process Effects 0.000 title abstract 2
- 238000003786 synthesis reaction Methods 0.000 title abstract 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 119
- 230000003197 catalytic effect Effects 0.000 claims abstract description 71
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims abstract description 24
- 239000000446 fuel Substances 0.000 claims abstract description 24
- 239000007788 liquid Substances 0.000 claims abstract description 17
- 239000003054 catalyst Substances 0.000 claims abstract description 13
- 239000007789 gas Substances 0.000 claims abstract description 13
- 239000002912 waste gas Substances 0.000 claims abstract description 6
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 27
- 239000002808 molecular sieve Substances 0.000 claims description 25
- 239000005977 Ethylene Substances 0.000 claims description 22
- 238000001704 evaporation Methods 0.000 claims description 16
- 230000008020 evaporation Effects 0.000 claims description 15
- 239000003344 environmental pollutant Substances 0.000 abstract description 2
- 231100000719 pollutant Toxicity 0.000 abstract description 2
- 238000011084 recovery Methods 0.000 abstract description 2
- 238000009834 vaporization Methods 0.000 abstract description 2
- 230000008016 vaporization Effects 0.000 abstract description 2
- 238000006555 catalytic reaction Methods 0.000 abstract 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract 1
- 238000007599 discharging Methods 0.000 abstract 1
- 239000003546 flue gas Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 6
- 238000010248 power generation Methods 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000006297 dehydration reaction Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000009825 accumulation Methods 0.000 description 2
- 238000000889 atomisation Methods 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 238000012271 agricultural production Methods 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000001131 transforming effect Effects 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02G—HOT GAS OR COMBUSTION-PRODUCT POSITIVE-DISPLACEMENT ENGINE PLANTS; USE OF WASTE HEAT OF COMBUSTION ENGINES; NOT OTHERWISE PROVIDED FOR
- F02G5/00—Profiting from waste heat of combustion engines, not otherwise provided for
- F02G5/02—Profiting from waste heat of exhaust gases
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/24—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by constructional aspects of converting apparatus
- F01N3/28—Construction of catalytic reactors
- F01N3/2882—Catalytic reactors combined or associated with other devices, e.g. exhaust silencers or other exhaust purification devices
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
- F02M31/00—Apparatus for thermally treating combustion-air, fuel, or fuel-air mixture
- F02M31/02—Apparatus for thermally treating combustion-air, fuel, or fuel-air mixture for heating
- F02M31/16—Other apparatus for heating fuel
- F02M31/18—Other apparatus for heating fuel to vaporise fuel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Exhaust Gas After Treatment (AREA)
Abstract
Description
技术领域technical field
本发明属于汽车节能减排的技术领域,特别是对发动机尾气余热重新吸收、转化、再利用的一种回收发动机排气管余热提高发动机综合油耗利用率的装置。The invention belongs to the technical field of automobile energy saving and emission reduction, in particular to a device for reabsorbing, transforming and reusing engine exhaust waste heat to recover engine exhaust pipe waste heat and improve engine comprehensive fuel consumption utilization rate.
背景技术Background technique
广泛使用乙醇汽油是我国乃至世界节能减排的方法之一,乙醇汽油是一种由粮食及各种植物纤维加工成的燃料乙醇和普通汽油按一定比例混和形成的新型替代能源。按照我国的国家标准,乙醇汽油是用90%的普通汽油与10%的燃料乙醇调和而成。使用乙醇汽油可节省石油资源,减少汽车尾气对空气的污染,还可促进农业的生产。但是乙醇汽油存在目前无法克服的缺点,首先,使用者最直观的感觉是它使汽车动力下降,不如普通汽油那么动力强劲,反而油耗增加,天热时还易于气阻熄火。另外由于乙醇汽油一旦遇水就会分层,无法采用成本很低的管道输送,乙醇汽油储运周期只有4—5天,这影响使用乙醇汽油的方便性。使用乙醇汽油的试验车进气阀上的堆积量要比使用93#无铅汽油的车平均高出33%。这是由于燃料乙醇的不稳定性造成发动机燃油进气系统上堆积物增加,使喷油嘴雾化不好、引起乙醇汽油燃烧效率下降,耗油量增加。Extensive use of ethanol gasoline is one of the methods of energy conservation and emission reduction in my country and the world. Ethanol gasoline is a new type of alternative energy that is formed by mixing fuel ethanol processed from grain and various plant fibers and ordinary gasoline in a certain proportion. According to my country's national standards, ethanol gasoline is blended with 90% regular gasoline and 10% fuel ethanol. The use of ethanol gasoline can save oil resources, reduce air pollution from vehicle exhaust, and promote agricultural production. However, ethanol gasoline has shortcomings that cannot be overcome at present. First, the most intuitive feeling for users is that it reduces the power of the car, which is not as powerful as ordinary gasoline. On the contrary, the fuel consumption increases. In addition, ethanol gasoline will be stratified once it meets water, so it cannot be transported by low-cost pipelines, and the storage and transportation period of ethanol gasoline is only 4-5 days, which affects the convenience of using ethanol gasoline. The amount of accumulation on the intake valve of the test car using ethanol gasoline is 33% higher than that of the car using 93# unleaded gasoline. This is because the instability of fuel ethanol increases the accumulation on the fuel intake system of the engine, which makes the atomization of the fuel injector poor, causing the combustion efficiency of ethanol gasoline to decrease, and the fuel consumption to increase.
目前对汽车尾气余热重新回收利用的方法主要是发电技术,最常见的方式是温差发电,由于温差发电片的热利用率不足5%,使得热能转化为电能的效率极低,更糟糕的是温差发电所发出的电压随温度变化较大,将电能储存到蓄电池中技术要求高且效率较低。还有一些专利中的奇思妙想是将火力发电系统小型化之后运用到汽车尾气余热的发电技术之中,首先,超大型火力发电厂的总效率不超过40%,所以该方法的实际热转化效率可想而知。At present, the method of recycling the waste heat of automobile exhaust is mainly power generation technology. The most common way is thermoelectric power generation. Since the heat utilization rate of the thermoelectric power generation sheet is less than 5%, the efficiency of converting heat energy into electrical energy is extremely low, and what is worse is the temperature difference. The voltage generated by power generation varies greatly with temperature, and storing electric energy in batteries requires high technical requirements and low efficiency. There are also some whimsical ideas in some patents that miniaturize the thermal power generation system and apply it to the power generation technology of automobile exhaust waste heat. First, the total efficiency of super-large thermal power plants does not exceed 40%, so the actual heat of this method The conversion efficiency can be imagined.
发明内容Contents of the invention
本发明的目的是针对上述问题提供提高发动机综合油耗利用率的装置一种回收发动机排气管余热提高发动机综合油耗利用率的装置,该装置能够对发动机尾气余热进行重新吸收、转化、再利用,同时为发动机提供双燃料,节约能源的同时能够大幅度降低尾气污染物的排放。The object of the present invention is to provide a device for improving the utilization rate of the comprehensive fuel consumption of the engine in view of the above problems, a device for recovering the waste heat of the exhaust pipe of the engine and improving the utilization rate of the comprehensive fuel consumption of the engine. At the same time, dual fuel is provided for the engine, which can greatly reduce the emission of exhaust pollutants while saving energy.
本发明的技术方案是:提高发动机综合油耗利用率的装置一种回收发动机排气管余热提高发动机综合油耗利用率的装置,包括乙醇供给装置A、乙醇催化装置B和乙烯供给装置C;The technical solution of the present invention is: a device for improving the comprehensive fuel consumption utilization rate of the engine, a device for recovering exhaust pipe waste heat of the engine and improving the comprehensive fuel consumption utilization rate of the engine, including an ethanol supply device A, an ethanol catalytic device B and an ethylene supply device C;
所述乙醇供给装置A包括乙醇箱和液泵;所述乙醇催化装置B包括蒸发器、蓄能器、气泵、催化器和排气歧管;所述乙烯供给装置C包括放水阀、分离器、进气歧管和发动机;The ethanol supply device A includes an ethanol tank and a liquid pump; the ethanol catalytic device B includes an evaporator, an accumulator, an air pump, a catalytic converter and an exhaust manifold; the ethylene supply device C includes a water discharge valve, a separator, intake manifold and engine;
所述催化器包括废气管和催化腔;所述蒸发器包括三元催化室和蒸发室;The catalytic converter includes an exhaust pipe and a catalytic chamber; the evaporator includes a three-way catalytic chamber and an evaporation chamber;
所述液泵安装在蒸发器及乙醇箱之间的连接管上;所述蒸发器的蒸发室、气泵、催化器的催化腔、分离器、进气歧管和发动机的进气口依次串联连接;所述蓄能器并联于蒸发器与气泵之间;所述放水阀连接于分离器底部;所述发动机的出气口、排气歧管、催化器的废气管、蒸发器的三元催化室依次串联连接。The liquid pump is installed on the connecting pipe between the evaporator and the ethanol tank; the evaporating chamber of the evaporator, the air pump, the catalytic chamber of the catalytic converter, the separator, the intake manifold and the air intake of the engine are sequentially connected in series The accumulator is connected in parallel between the evaporator and the air pump; the water discharge valve is connected to the bottom of the separator; sequentially connected in series.
上述方案中,所述催化器为环形,中间为废气管、外圆为催化腔,废气管和催化腔完全隔开;In the above solution, the catalytic converter is ring-shaped, the middle is an exhaust gas pipe, and the outer circle is a catalytic chamber, and the exhaust gas pipe and the catalytic chamber are completely separated;
所述催化腔的一端设有乙醇进气口,另一端设有乙烯出气口、且两端均设有催化剂进口,分子筛从两端的催化剂进口装入后通过盖板密封盖紧。One end of the catalytic chamber is provided with an ethanol inlet, the other end is provided with an ethylene outlet, and both ends are provided with a catalyst inlet, and molecular sieves are loaded from the catalyst inlets at both ends and sealed tightly by a cover plate.
上述方案中,所述催化器还包括导流板,所述导流板安装在催化腔内。In the above solution, the catalytic converter further includes a deflector, and the deflector is installed in the catalytic chamber.
上述方案中,所述分子筛为HZSM-5分子筛、beta分子筛、ZSM-35分子筛或3A/4A/5A分子筛中的任意一种。In the above scheme, the molecular sieve is any one of HZSM-5 molecular sieve, beta molecular sieve, ZSM-35 molecular sieve or 3A/4A/5A molecular sieve.
上述方案中,所述分子筛为HZSM-5分子筛。In the above scheme, the molecular sieve is HZSM-5 molecular sieve.
上述方案中,所述蒸发器包括三元催化器和蒸发室;In the above scheme, the evaporator includes a three-way catalytic converter and an evaporation chamber;
所述三元催化器内设有三元催化室,三元催化室与蒸发室完全隔开的,所述蒸发室的一端设有进液口,另一端设有出气口。The three-way catalytic converter is provided with a three-way catalytic chamber, which is completely separated from the evaporation chamber. One end of the evaporation chamber is provided with a liquid inlet, and the other end is provided with a gas outlet.
上述方案中,还包括溢流阀;所述溢流阀并联于蒸发器和乙醇箱之间。In the above solution, an overflow valve is also included; the overflow valve is connected in parallel between the evaporator and the ethanol tank.
上述方案中,所述分离器底部设有放水阀。In the above solution, a drain valve is provided at the bottom of the separator.
与现有技术相比,本发明的有益效果是:Compared with prior art, the beneficial effect of the present invention is:
1、本发明采用以上技术方案,能够大幅度降低发动机的排气热负荷,显著延长排气歧管的使用寿命,同时还能有效降低排气噪声,提高乘坐舒适性。1. The present invention adopts the above technical solutions, which can greatly reduce the exhaust heat load of the engine, significantly prolong the service life of the exhaust manifold, effectively reduce exhaust noise, and improve ride comfort.
2、本发明采用的是将低热值的乙醇经过吸热、催化、脱水之后转化为高热值的乙烯,并将制备的乙烯参与到发动机的燃烧系统中去,采用乙醇和汽油分开携带的方案,能够有效解决乙醇汽油储存周期短、供油系统严格的问题;由于没有将乙醇直接参与到燃烧系统中去,故不会出现乙醇雾化差与堵塞管道的问题;乙烯的折合热值与汽油热值相当,不会出现向使用乙醇汽油那样使发动机功率下降的现象。2. The present invention adopts the method that ethanol with low calorific value is converted into ethylene with high calorific value after endothermic, catalyzed, and dehydrated, and the prepared ethylene is used in the combustion system of the engine, and the ethanol and gasoline are carried separately. It can effectively solve the problems of short ethanol gasoline storage period and strict oil supply system; since ethanol is not directly involved in the combustion system, there will be no problems of poor atomization of ethanol and blocked pipes; the equivalent calorific value of ethylene and the heat of gasoline The value is equivalent, and there will be no phenomenon that the engine power will be reduced like the use of ethanol gasoline.
3、本发明采用的是从排气余热中提供乙醇催化脱水所需的反应热量,可以显著提高发动机的综合热效率,将尾气余热直接储存在乙烯的化学能之中,省去了热能转化为电能或其他动能的中间低效率环节,大大提高能量回收利用的效率。3. The present invention adopts the heat of reaction required for ethanol catalytic dehydration from exhaust waste heat, which can significantly improve the overall thermal efficiency of the engine, and directly store the waste heat of exhaust gas in the chemical energy of ethylene, eliminating the need to convert heat energy into electric energy Or other intermediate low-efficiency links of kinetic energy, greatly improving the efficiency of energy recovery and utilization.
4、本方案的催化器还可以与排气歧管做成一体,乙醇催化脱水反应是吸热反应,相当于对排气歧管配备了降温系统,那么排气歧管可以采用薄壁设计,对汽车轻量化有一定的贡献。4. The catalytic converter of this solution can also be integrated with the exhaust manifold. The catalytic dehydration reaction of ethanol is an endothermic reaction, which is equivalent to a cooling system for the exhaust manifold, so the exhaust manifold can be designed with thin walls. It has a certain contribution to the lightweight of automobiles.
附图说明Description of drawings
图1:是本发明一实施方式的整体结构布置图;Fig. 1: is the overall structural arrangement diagram of an embodiment of the present invention;
图2:是本发明一实施方式的蒸发器正面结构示意图;Figure 2: It is a schematic diagram of the front structure of an evaporator according to an embodiment of the present invention;
图3:是图2A-A剖视图;Figure 3: is a sectional view of Figure 2A-A;
图4:是本发明一实施方式的蒸发器侧面机构示意图;Figure 4: is a schematic diagram of the side mechanism of the evaporator according to an embodiment of the present invention;
图5:是本发明一实施方式的催化器结构示意图;Fig. 5: is a schematic structural diagram of a catalytic converter according to an embodiment of the present invention;
图6:是图5B-B剖视图;Figure 6: is a sectional view of Figure 5B-B;
图7:是图5D-D剖视图;Figure 7: is a sectional view of Figure 5D-D;
图8:是本发明一实施方式的催化器装配正面图;Fig. 8: is the assembly front view of the catalytic converter of one embodiment of the present invention;
图9:是本发明一实施方式的催化器装配侧面图;Figure 9: It is a side view of the assembly of the catalytic converter according to one embodiment of the present invention;
图10:是本发明一实施方式的催化器装配爆炸图。Fig. 10 is an exploded view of the assembly of the catalytic converter according to one embodiment of the present invention.
图中:1、发动机;2、进气歧管;3、分离器;4、放水阀;5、排气歧管;6、催化器;601、废气管;6011、排气腔;602、乙醇进气口;603、乙烯出气口;604、导流板;605、螺纹孔;606、催化腔;607、催化剂进口;608、分子筛;609、螺钉;610、盖板;611、密封垫片;7、气泵;8、蓄能器;9、蒸发器;901、进液口;902、三元催化器;903、出气口;904、三元催化室;905、蒸发室;10、溢流阀;11、液泵;12、乙醇箱。In the figure: 1. engine; 2. intake manifold; 3. separator; 4. drain valve; 5. exhaust manifold; 6. catalytic converter; 601. exhaust pipe; 6011. exhaust cavity; 602. ethanol Air inlet; 603, ethylene outlet; 604, deflector; 605, threaded hole; 606, catalytic chamber; 607, catalyst inlet; 608, molecular sieve; 609, screw; 610, cover plate; 611, sealing gasket; 7. Air pump; 8. Accumulator; 9. Evaporator; 901. Liquid inlet; 902. Three-way catalytic converter; 903. Air outlet; 904. Three-way catalytic chamber; 905. Evaporation chamber; 10. Overflow valve ; 11. Liquid pump; 12. Ethanol tank.
具体实施方式detailed description
下面结合附图和具体实施方式对本发明作进一步详细说明,但本发明的保护范围并不限于此。The present invention will be described in further detail below in conjunction with the accompanying drawings and specific embodiments, but the protection scope of the present invention is not limited thereto.
图1所示为本发明所述回收发动机排气管余热提高发动机综合油耗利用率的装置的一种实施方式,现有的汽车技术,汽车发动机1在正常稳定工作后,排气歧管5温度在600℃以上,而本发明带有三元催化器的蒸发器9温度在300℃以上。该装置采用发动机废气余热使乙醇脱水制备乙烯,再将乙烯参与到燃烧系统中去。所述回收发动机排气管余热提高发动机综合油耗利用率的装置,包括乙醇供给装置A、乙醇催化装置B和乙烯供给装置C。Fig. 1 shows an embodiment of the device for recovering engine exhaust pipe waste heat of the present invention and improving the comprehensive fuel consumption utilization rate of the engine. In the existing automobile technology, after the automobile engine 1 works normally and stably, the temperature of the exhaust manifold 5 Above 600°C, while the temperature of the evaporator 9 with the three-way catalytic converter of the present invention is above 300°C. The device uses the waste heat of engine exhaust gas to dehydrate ethanol to prepare ethylene, and then participates in the combustion system with ethylene. The device for recovering waste heat from the exhaust pipe of the engine to improve the utilization rate of the comprehensive fuel consumption of the engine includes an ethanol supply device A, an ethanol catalytic device B and an ethylene supply device C.
所述乙醇供给装置A包括乙醇箱12、液泵11和溢流阀10;所述液泵11安装在蒸发器9及乙醇箱12之间的连接管上;所述溢流阀10并联于蒸发器9和乙醇箱12之间。The ethanol supply device A includes an ethanol tank 12, a liquid pump 11 and an overflow valve 10; the liquid pump 11 is installed on the connecting pipe between the evaporator 9 and the ethanol tank 12; the overflow valve 10 is connected in parallel to the evaporator Between the device 9 and the ethanol tank 12.
所述乙醇催化装置B包括蒸发器9、蓄能器8、气泵7、催化器6和排气歧管5。The ethanol catalytic device B includes an evaporator 9 , an accumulator 8 , an air pump 7 , a catalytic converter 6 and an exhaust manifold 5 .
如图2、3和4所示,所述蒸发器9包括三元催化器902和蒸发室905;所述三元催化器902内设有三元催化室904,三元催化室904与蒸发室905完全隔开的,所述蒸发室905的一端设有进液口901,另一端设有出气口903。As shown in Figures 2, 3 and 4, the evaporator 9 includes a three-way catalytic converter 902 and an evaporation chamber 905; Completely separated, one end of the evaporation chamber 905 is provided with a liquid inlet 901 , and the other end is provided with an air outlet 903 .
如图5、6和7所示,所述催化器6为环形,中间为废气管601、外圆为催化腔606,废气管601和催化腔606完全隔开;所述催化腔606的一端设有乙醇进气口602,另一端设有乙烯出气口603、且两端均设有催化剂进口607,分子筛608从两端的催化剂进口607装入后依次通过密封垫片611和盖板610一起将催化器进口密封住,最后拧上螺钉609,如图8、9、和10所示。所述催化器6还包括导流板604,所述导流板604安装在催化腔606内,乙醇蒸汽在导流板604的引导下,在600℃左右的催化器6内呈S型前进,让乙醇有更长的行走距离,与催化剂有更长的接触时间,催化更加充分。As shown in Figures 5, 6 and 7, the catalytic converter 6 is annular, the middle is a waste gas pipe 601, and the outer circle is a catalytic chamber 606, and the waste gas pipe 601 and the catalytic chamber 606 are completely separated; one end of the catalytic chamber 606 is provided There is an ethanol inlet 602, the other end is provided with an ethylene outlet 603, and both ends are provided with catalyst inlets 607, and molecular sieves 608 are loaded from the catalyst inlets 607 at both ends, and the catalytic The inlet of the device is sealed, and finally the screw 609 is screwed on, as shown in Figures 8, 9 and 10. The catalytic converter 6 also includes a deflector 604, which is installed in the catalytic chamber 606. Under the guidance of the deflector 604, the ethanol vapor advances in an S shape in the catalytic converter 6 at about 600°C. Let the ethanol have a longer walking distance, have a longer contact time with the catalyst, and catalyze more fully.
所述分子筛608为HZSM-5分子筛、beta分子筛、ZSM-35分子筛或3A/4A/5A分子筛中的任意一种。优选的,所述分子筛608为HZSM-5分子筛。The molecular sieve 608 is any one of HZSM-5 molecular sieve, beta molecular sieve, ZSM-35 molecular sieve or 3A/4A/5A molecular sieve. Preferably, the molecular sieve 608 is HZSM-5 molecular sieve.
所述乙烯供给装置C包括放水阀4、分离器3、进气歧管2和发动机1。所述分离器3底部设有放水阀4。The ethylene supply device C includes a drain valve 4 , a separator 3 , an intake manifold 2 and an engine 1 . The bottom of the separator 3 is provided with a drain valve 4 .
所述蒸发器9的蒸发室905、气泵7、催化器6的催化腔606、分离器3、进气歧管2和发动机1的进气口依次串联连接;所述蓄能器8并联于蒸发器9与气泵7之间;所述放水阀4连接于分离器3底部;所述发动机1的出气口、排气歧管5、催化器6的废气管601、蒸发器9的三元催化室904依次串联连接。其中,所述放水阀4、气泵7和液泵11均为电子控制器件。The evaporation chamber 905 of the evaporator 9, the air pump 7, the catalytic chamber 606 of the catalytic converter 6, the separator 3, the intake manifold 2 and the intake port of the engine 1 are sequentially connected in series; the accumulator 8 is connected in parallel to the evaporation Between the device 9 and the air pump 7; the water discharge valve 4 is connected to the bottom of the separator 3; the air outlet of the engine 1, the exhaust manifold 5, the waste gas pipe 601 of the catalytic converter 6, and the three-way catalytic chamber of the evaporator 9 904 are sequentially connected in series. Wherein, the water discharge valve 4, the air pump 7 and the liquid pump 11 are all electronic control devices.
整个乙烯催化系统需要做隔热保温,在表面涂上一层隔热涂层。。The entire ethylene catalytic system needs to be insulated and heat-insulated, and a layer of heat-insulating coating should be coated on the surface. .
本发明的工作过程为:Working process of the present invention is:
在发动机1正常稳定工作之后,液泵11从乙醇箱12中抽取一定量的液体乙醇从进液口901进入蒸发室905,液体乙醇在300℃下变为乙醇蒸汽从出气口903进入管道和蓄能器8,气泵7匀速地泵入适量的乙醇蒸气到从催化器6的乙醇进气口602进入到催化腔606中,乙醇蒸汽在导流板604的引导下,在600℃左右的催化器6内呈S型前进,并被催化剂HZSM-5分子筛608催化脱水成乙烯,然后从乙烯出气口603导出经过管道导入分离器3,由于乙烯不溶于水,在分离器内将乙烯依次洗气、干燥并经过导管通入至进气歧管2内,发动机1进气时将乙烯混合空气一起吸入气缸内,发动机1完成燃烧之后从排气歧管5将高温废气排出,高温废气进入三元催化器902的三元催化室904中,将有害气体变成无害气体,使汽车尾气得以净化。通过高温废气为乙醇汽化及催化脱水提供源源不断的热量。通过这一套装置达到发动机节能减排、降低噪声效益。After the engine 1 works normally and stably, the liquid pump 11 extracts a certain amount of liquid ethanol from the ethanol tank 12 and enters the evaporation chamber 905 through the liquid inlet 901, and the liquid ethanol becomes ethanol vapor at 300° C. Energizer 8 and air pump 7 pump an appropriate amount of ethanol vapor at a constant speed to enter the catalytic chamber 606 from the ethanol inlet 602 of the catalytic converter 6. 6 advances in an S-shape, and is catalyzed by the catalyst HZSM-5 molecular sieve 608 to dehydrate into ethylene, and then it is exported from the ethylene outlet 603 through a pipeline and introduced into the separator 3. Since ethylene is insoluble in water, the ethylene is washed in sequence in the separator, It is dried and passed into the intake manifold 2 through the duct. When the engine 1 is inhaled, the ethylene mixed air is sucked into the cylinder together. After the engine 1 completes the combustion, the high-temperature exhaust gas is discharged from the exhaust manifold 5, and the high-temperature exhaust gas enters the three-way catalyst. In the three-way catalytic chamber 904 of the device 902, the harmful gas is changed into a harmless gas, so that the exhaust gas of the automobile can be purified. The high-temperature exhaust gas provides continuous heat for ethanol vaporization and catalytic dehydration. Through this set of devices, the benefits of energy saving, emission reduction and noise reduction of the engine can be achieved.
应当理解,虽然本说明书是按照各个实施例描述的,但并非每个实施例仅包含一个独立的技术方案,说明书的这种叙述方式仅仅是为清楚起见,本领域技术人员应当将说明书作为一个整体,各实施例中的技术方案也可以经适当组合,形成本领域技术人员可以理解的其他实施方式。It should be understood that although this description is described according to various embodiments, not each embodiment only includes an independent technical solution, and this description of the description is only for clarity, and those skilled in the art should take the description as a whole , the technical solutions in the various embodiments can also be properly combined to form other implementations that can be understood by those skilled in the art.
上文所列出的一系列的详细说明仅仅是针对本发明的可行性实施例的具体说明,它们并非用以限制本发明的保护范围,凡未脱离本发明技艺精神所作的等效实施例或变更均应包含在本发明的保护范围之内。The series of detailed descriptions listed above are only specific descriptions for feasible embodiments of the present invention, and they are not intended to limit the protection scope of the present invention. Any equivalent embodiment or All changes should be included within the protection scope of the present invention.
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JPS5575491A (en) * | 1978-12-04 | 1980-06-06 | Hiromi Ikeda | Producing liquid fuel for power source by subjecting alcohol to chemical change |
US4475484A (en) * | 1981-02-27 | 1984-10-09 | Filho Antonio V | Exhaust manifold for an internal combustion engine, apparatus for the catalytic transformation of fuel and improved internal combustion engine |
CN1252490A (en) * | 1998-10-23 | 2000-05-10 | 梅塞尔·格里斯海姆有限公司 | Ethylene use and method for driving IC engine |
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Publication number | Priority date | Publication date | Assignee | Title |
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JPS5575491A (en) * | 1978-12-04 | 1980-06-06 | Hiromi Ikeda | Producing liquid fuel for power source by subjecting alcohol to chemical change |
US4475484A (en) * | 1981-02-27 | 1984-10-09 | Filho Antonio V | Exhaust manifold for an internal combustion engine, apparatus for the catalytic transformation of fuel and improved internal combustion engine |
CN1252490A (en) * | 1998-10-23 | 2000-05-10 | 梅塞尔·格里斯海姆有限公司 | Ethylene use and method for driving IC engine |
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